CN202303332U - Drainage waste heat recycling system - Google Patents

Drainage waste heat recycling system Download PDF

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Publication number
CN202303332U
CN202303332U CN2011203632560U CN201120363256U CN202303332U CN 202303332 U CN202303332 U CN 202303332U CN 2011203632560 U CN2011203632560 U CN 2011203632560U CN 201120363256 U CN201120363256 U CN 201120363256U CN 202303332 U CN202303332 U CN 202303332U
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CN
China
Prior art keywords
water
steam
tank
drainage
exhaust port
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2011203632560U
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Chinese (zh)
Inventor
焦培迅
龙万青
刘尚军
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Jinan Qiquan Thermoelectricity Co Ltd
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Jinan Qiquan Thermoelectricity Co Ltd
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Filing date
Publication date
Application filed by Jinan Qiquan Thermoelectricity Co Ltd filed Critical Jinan Qiquan Thermoelectricity Co Ltd
Priority to CN2011203632560U priority Critical patent/CN202303332U/en
Application granted granted Critical
Publication of CN202303332U publication Critical patent/CN202303332U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses a drainage waste heat recycling system, which comprises at least one flash tank, an energy collector and a drainage tank, wherein the water outlet of the flash tank is communicated with the drainage tank; water-sealing devices are arranged on the flash tank and the steam exhaust port of the drainage tank; a steam pipeline is arranged between the steam exhaust port and the water-sealing device; the drainage tank is provided with a steam pipeline; and the steam pipeline is communicated with the energy collector. In the system, a water-sealing device is arranged on the steam exhaust port of each flash tank, a steam pipeline is connected between the steam exhaust port of each drainage flash tank and a water seal, steam exhausted to the atmospheric air is led to the energy collector, steam is mixed with unit condensed water in the energy collector and absorbs energy to generate high-temperature water, and he high-temperature water enters the drainage tank and enters a de-aerator through a water pump, so that the aim of comprehensively utilizing is fulfilled; and according to calculation, the recovery benefit is very considerable.

Description

A kind of hydrophobic heat recovery system
Technical field
The utility model relates to a kind of hydrophobic heat recovery system.
Background technology
As everyone knows, thermoelectric industry unit peak valley operation, the start-stop of equipment switching device is very frequent; In therrmodynamic system,, carry out heating coil as long as there have equipment switching and start and stop just to need to open pipeline to be hydrophobic; Hydrophobic must opening before equipment does not reach rated temperature and pressure, great amount of heat is carried in all hydrophobic meetings, and the hydrophobic hot break value of medium temperature and medium pressure is up to 1400KJ/kg; Owing to can not reclaim, can only carry out emptying, cause a large amount of wastes and noise.And local steam power plant thermic load is unstable, causes the deaerator level fluctuation bigger, and demineralized water was nervous when thermic load was high, and when load was low, the high outwards spilling water of deaerator level if do not reclaim spilling water, will cause the significant wastage of demineralized water.Add holding at high price of coal, local thermoelectric industry is suffered untold misery, scrap build, the energy-conservation unique selection of having taped the latent power and having reduced cost into local thermoelectric enterprise.
Summary of the invention
To above-mentioned prior art; The utility model provides a kind of hydrophobic heat recovery system, and it is that the inventor is actual according to the equipment of oneself, to the hydrophobic transformation of carrying out of heat power equipment; Various hydrophobic; The pipeline such as oxygen-eliminating device spilling water that promptly discharges water is connected in the container, reaches the purpose that reclaims demineralized water, and retrieves to heat demineralized water through steam preheating and reach energy saving purposes.
The utility model is realized through following technical scheme:
A kind of hydrophobic heat recovery system; Comprise at least one flash vessel, receive ability device and drain tank, wherein, the discharge outlet of flash vessel is communicated with drain tank; The steam drain place of flash vessel and drain tank is provided with water seal arrangement; Be provided with jet chimney between steam drain and the water seal arrangement, also be provided with jet chimney on the drain tank, jet chimney can be communicated with by device with receipts.
During use; According to different equipment pressure ratings, heat distribution pipeline hydrophobic is divided into different hydrophobic female pipes, with the unified flash vessel that is connected to different brackets of hydrophobic female pipe; Drain tank is communicated with oxygen-eliminating device; Establish two drainage pumps (fortune one is equipped with) on the connecting pipeline, simultaneously the oxygen-eliminating device spilling water is connected to drain tank, will receive and to be communicated with unit condensate or demineralized water pipeline by device.During work, the water in the heat distribution pipeline drains in the drain tank and reclaims, and steam then gets into through jet chimney and receives the ability device; Unit condensate or demineralized water also get into receipts ability device simultaneously, and the ability device is inner receiving, the steam that steam turbine condensate or demineralized water cooling are got into; Through receiving inner atomising device, the dehydration plate of ability device; Make the abundant and vapor mixing of condensate or demineralized water, the heating demineralized water, and reach purpose energy-conservation and the elimination thermal loss; Condensate after heating or demineralized water get into drain tank then, are driven into oxygen-eliminating device through drainage pump, behind oxygen-eliminating device, get into boiler through feed pump again and use.So, promptly recyclable a large amount of demineralized water also can reclaim the steam preheating that flash vessel is arranged, and also can heat demineralized water through recovered steam, and through measuring and calculating, the demineralized water temperature can improve about 20 ℃.
For letting the steam discharge of each flash vessel get into receipts ability device smoothly, the inventor of the utility model has done a lot of experiments, and each steam drain can not add door; Pressure is too high when preventing that equipment from operating suddenly, can normal emptying be unlikely to support bad water tank for guaranteeing steam, and can reclaim each steam discharge at ordinary times; The inventor is installed water seal arrangement according to water-seal principle additional at each steam drain place, can guarantee the recovery of pressure vapour; Can guarantee the safety of equipment again, through the operation of some months, through the check of various operating modes; Scrap build is extremely successful, reaches its intended purposes.
The utility model is installed water seal arrangement at each flash vessel steam drain, is connected jet chimney between the steam drain of each dewatering capacity-enlarging device and the water seal, and guiding to receipts to row to the steam of atmosphere can device; Steam receive mixes with the unit condensate in can device receive ability after, produce high-temperature water, high-temperature water entering drain tank; High-temperature water gets into oxygen-eliminating device through water pump then; Reach the purpose of comprehensive utilization, through calculating, it is considerable to reclaim benefit.
Description of drawings
Fig. 1 is the structural representation of the utility model;
Fig. 2 is the workflow sketch map (arrow is represented the flow direction of water or steam among the figure) of the utility model.
Wherein, 1, flash vessel; 2, drain tank; 3, water seal arrangement; 4, receive the ability device; 5, the high pressure flash vessel that promptly discharges water; 6, high pressure dewatering capacity-enlarging device; 7, middle pressure dewatering capacity-enlarging device; 8, water seal; 9, trench; 10, the urgent waterproof of high-pressure boiler; 11, the high-pressure boiler system is hydrophobic; 12, the medium-pressure boiler system is hydrophobic; 13, unit condensate or demineralized water; 14, oxygen-eliminating device spilling water; 15, remove oxygen-eliminating device; 16, afterheat steam.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is further described.
A kind of hydrophobic heat recovery system comprises several flash vessels, receiving can device and drain tank, as shown in Figure 1; Wherein, The discharge outlet of flash vessel is communicated with drain tank, and the steam drain place of flash vessel and drain tank is provided with water seal arrangement (water seal arrangement is a structure conventional in the prior art), is provided with jet chimney between steam drain and the water seal arrangement; Also be provided with jet chimney on the drain tank, jet chimney can be communicated with by device with receipts.
During use; According to different equipment pressure ratings, heat distribution pipeline hydrophobic is divided into different hydrophobic female pipes, with the unified flash vessel that is connected to different brackets of hydrophobic female pipe; Drain tank is communicated with oxygen-eliminating device; Establish two drainage pumps (fortune one is equipped with) on the connecting pipeline, simultaneously the oxygen-eliminating device spilling water is connected to drain tank, will receive and to be communicated with unit condensate or demineralized water pipeline by device.During work, the water in the heat distribution pipeline drains in the drain tank and reclaims, and steam then gets into through jet chimney and receives the ability device; Unit condensate or demineralized water also get into receipts ability device simultaneously, and the ability device is inner receiving, the steam that steam turbine condensate or demineralized water cooling are got into; Through receiving inner atomising device, the dehydration plate of ability device; Make the abundant and vapor mixing of condensate or demineralized water, the heating demineralized water, and reach purpose energy-conservation and the elimination thermal loss; Condensate after heating or demineralized water get into drain tank then, are driven into oxygen-eliminating device through drainage pump, behind oxygen-eliminating device, get into boiler through feed pump again and use.So, promptly recyclable a large amount of demineralized water also can reclaim the steam preheating that flash vessel is arranged, and also can heat demineralized water through recovered steam, and through measuring and calculating, the demineralized water temperature can improve about 20 ℃.
The utility model is installed water seal arrangement at each flash vessel steam drain, is connected jet chimney between the steam drain of each dewatering capacity-enlarging device and the water seal, and guiding to receipts to row to the steam of atmosphere can device; Steam receive mixes with the unit condensate in can device receive ability after, produce high-temperature water, high-temperature water entering drain tank; High-temperature water gets into oxygen-eliminating device through water pump then; Reach the purpose of comprehensive utilization, through calculating, it is considerable to reclaim benefit: demineralized water reclaims by per hour reclaiming the en demineralized water and calculates; Every side's demineralized water cost is 3 yuan, ten thousand yuan of then annual recyclable demineralized water 24 * 0.5 * 3 * 8000=28.8.The recovered steam waste heat; Press per hour recovered steam 1000kg, temperature can be practiced thrift coal-fired 1000 * 2875.4kj/kg ÷ 29302kj/kg * 8000h=785.03 ton year by 200 ℃ of calculating; Mark coal per ton is by 800 yuan of calculating, and year can economize on the use of funds: ten thousand yuan of 785.03 * 800=62.8024.Ten thousand yuan of 28.8+62.8=91.6 can economize on the use of funds in whole therrmodynamic system waste heat recovery year.Investment is no more than 200,000 yuan, and a season is with regard to recovery cost, considerable benefit.

Claims (1)

1. hydrophobic heat recovery system; It is characterized in that: comprise at least one flash vessel, receive ability device and drain tank, wherein, the discharge outlet of flash vessel is communicated with drain tank; The steam drain place of flash vessel and drain tank is provided with water seal arrangement; Be provided with jet chimney between steam drain and the water seal arrangement, also be provided with jet chimney on the drain tank, jet chimney can be communicated with by device with receipts.
CN2011203632560U 2011-09-26 2011-09-26 Drainage waste heat recycling system Expired - Fee Related CN202303332U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011203632560U CN202303332U (en) 2011-09-26 2011-09-26 Drainage waste heat recycling system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011203632560U CN202303332U (en) 2011-09-26 2011-09-26 Drainage waste heat recycling system

Publications (1)

Publication Number Publication Date
CN202303332U true CN202303332U (en) 2012-07-04

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Application Number Title Priority Date Filing Date
CN2011203632560U Expired - Fee Related CN202303332U (en) 2011-09-26 2011-09-26 Drainage waste heat recycling system

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105180142A (en) * 2015-09-02 2015-12-23 华北电力科学研究院有限责任公司 System and method for recovering drain water and steam of soot-blowing warming pipe
CN108167807A (en) * 2018-01-02 2018-06-15 武汉都市环保工程技术股份有限公司 Garbage incinerating power plant steam air heater draining system
CN111482061A (en) * 2020-04-10 2020-08-04 龙净科杰环保技术(上海)有限公司 Device and method for recycling drainage of urea denitration system of coal-fired unit

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105180142A (en) * 2015-09-02 2015-12-23 华北电力科学研究院有限责任公司 System and method for recovering drain water and steam of soot-blowing warming pipe
CN105180142B (en) * 2015-09-02 2017-05-31 华北电力科学研究院有限责任公司 A kind of soot blowing heating coil hydrophobic and steam recovery system and method
CN108167807A (en) * 2018-01-02 2018-06-15 武汉都市环保工程技术股份有限公司 Garbage incinerating power plant steam air heater draining system
CN108167807B (en) * 2018-01-02 2024-03-19 中冶南方都市环保工程技术股份有限公司 Drainage system of steam-air preheater of garbage incineration power plant
CN111482061A (en) * 2020-04-10 2020-08-04 龙净科杰环保技术(上海)有限公司 Device and method for recycling drainage of urea denitration system of coal-fired unit

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GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120704

Termination date: 20190926